• 대한기계학회:학술대회논문집
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• 대한기계학회 2007년도 춘계학술대회B
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• pp.2817-2822
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• 2007

The purpose of this paper is to study the influence of operating condition and ejector geometries on the hydrodynamics and on the mass transfer characteristic of ejector. The CFD results were validated with available experimental data. Flow field analyses and predictions of ejector performance were also carried out. Variation on the operating conditions was made by varying the gas-liquid flow rate ratio in the range of 0.2 to 1.2. The ejector configuration was also varied on the length to diameter ratio of mixing tube ($L_M/D_M$) in the range of 4 to 10. CFD studies show that at $L_M/D_M$ 5.5, the volumetric mass transfer coefficient increases with respect to gas flow rates. Meanwhile, at $L_M/D_M$ 4, the plot of volumetric mass transfer coefficient to gas-liquid flow rates ratio reach maximum at gas-liquid flow rates ratio of 0.6. This study also shows that volumetric mass transfer coefficient decrease with respect to the increase of mixing tube length.

• 대한기계학회:학술대회논문집
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• 대한기계학회 2007년도 춘계학술대회B
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• pp.2708-2713
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• 2007

The aim of this paper is further studies to achieve deeper understanding in this field. First investigate the influence of operating conditions and design parameters on the hydrodynamics and the mass transfer properties of a loop reactor. This paper provides a literature review on the ejectors applications in the mixing system. A number of studies are grouped and discussed in several topics such as the background, theory of ejector, mixing characteristics, optimization of the system. Since the high efficiencies reactor using ejector widely used in gas-liquid system, especially in a number of chemical and biochemical processes. This is due to their high efficiency in gas dispersion resulting in high mass transfer rate and low power requirements. Thus ejector has been applied to the mixing system. An investigation on hydrodynamics and mass transfer characteristics of gas-liquid ejector has been carried out using three-dimensional CFD modeling.

• 한국가시화정보학회지
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• 제11권1호
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• pp.34-40
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• 2013

Gas/liquid two-phase ejector is a device without moving parts, in which liquid is used to drive gas of a low-pressure source. In this paper, the hydrodynamic characteristics of a vertical down type two-phase ejector were studied using an air-water loop system. Entrained air flow rates were measured with inlet and outlet pressures of the ejector with varying water flow rate. Homogeneous bubbly flows in the discharge pipe were confirmed by the high speed flow visualization method. Quantitative measurements of void fraction were made using a newly developed fiber optic probe system.

• 대한기계학회논문집B
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• 제39권2호
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• pp.183-190
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• 2015

무동력펌프의 일종인 이젝터는 압력을 갖는 유체를 노즐에서 분사하여 주위의 유체를 흡입 후 혼합유체를 외부 동력 없이 송출하는 장치이다. 구조가 간단하고 고장이 적어 여러 산업분야에서 이용되고 있으며, 자동차 산업에서는 연료주입용으로도 이용되고 있다. 대부분 이젝터는 가스상을 사용하기 때문에, 가스상 이젝터는 오래전부터 연구되어 왔다. 액체상 이젝터는 그 용도에 비해 아직 연구가 활발하지 못하다. 가스상 이젝터와 달리, 액체상 이젝터는 노즐목에서 부분적인 압력강하에의한 공동현상이 발생되고 이러한 공동현상은 부품파손을 유발하며, 소음을 발생시키는 원인이 되고 있다. 본 연구는 액체-액체상 이젝터의 최대 유량비와 공동현상 발생영역 비교를 위해 5가지 인자를 변경하여 2차원 축대칭 전산해석을 진행하였다. 액체 이젝터의 공동현상에서는 특히 노즐각도가 중요한 역할을 하였으며, 유량비 성능 특성은 혼합챔버각도 $35^{\circ}$가 가장 유리한 것으로 판단된다. 이를 통해 공동 현상을 최소화시키면서 성능 최적화를 달성할 수 있는 조합을 얻을 수 있음을 확인하였다.

• 한국기계가공학회지
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• 제11권6호
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• pp.189-194
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• 2012

The purpose of this study is to predict the performance of a cyclone drying machine and air ejector used in drying applications. This paper deals with optimization of the geometry of the ejector for sludge drying using computational fluid dynamics. To facilitate the design of a jet ejector for air drying machines, a numerical model of simultaneous mass and heat transfers between the liquid(sludge) and gas(air) phases in the jet ejector was developed. The steady-state model was based on unidimensional balance equations of mass, energy and momentum for the liquid and gas phases. It was shown that the optimum condition to minimize pressure and momentum loss of air in the ejector was d=220mm. It was found that sludge particles inside the cyclone was smoothly discharged by the conical wedge installed on the bottom of the cyclone.

• 한국태양에너지학회 논문집
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• 제31권3호
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• pp.23-28
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• 2011

In this study, the ejector design was modeled using Fluent 6.3 of FVM(Finite Volume Method) CFD(Computational Fluid Dynamics) techniques to resolve the flow dynamics in the ejector. A vacuum system with the ejector has been widely used because of its simple construction and easy maintenance. Ejector is the main part of the desalination system, of which designs determine the efficiency of system. The effects of the ejector was investigated geometry and the operating conditions in the hydraulic characteristics. The ejector consists mainly of a nozzle, suction chamber, mixing tube (throat), diffuser and draft tube. Liquid is supplied to the ejector nozzle, the fast liquid jet produced by the nozzle entrains and the non condensable gas was sucked into the mixing tube. The multiphase CFD modeling was carried out to determine the hydrodynamic characteristics of seawater-air ejector. Condition of the simulation was varied in entrance mass flow rate (1kg/s, 1.5kg/s, 2kg/s, 2.5kg/s, 3kg/s), and position of driving nozzle was located from the central axis of the suction at -10mm, 0mm, 10mm, 20mm, 30mm.. Asaresult, suction flow velocity has the highest value in central axis of the suction.

• 한국태양에너지학회 논문집
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• 제30권6호
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• pp.137-143
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• 2010

In this study, the ejector design was modeled using Fluent 6.3 of FVM(Finite Volume Method) CFD(Computational Fluid Dynamics) techniques to resolve the flow dynamics in the ejector. A vacuum system with the ejector has been widely used because of its simple construction and easy maintenance. Ejector is the main part of the desalination system, of which designs determine the efficiency of system. The effects of the ejector was investigated geometry and the operating conditions in the hydraulic characteristics. The ejector consists mainly of a nozzle, suction chamber, mixing tube(throat), diffuser and draft tube. Liquid is supplied to the ejector nozzle, the fast liquid jet produced by the nozzle entrains and the non condensable gas was sucked into the mixing tube. In the present study, the multiphase CFD modeling was carried out to determine the hydrodynamic characteristics of seawater-air ejector. Two-dimensional geometry was considered with the quadrilateral-mashing scheme. The gas suction rate increases with increasing Motive flow circulating rate.

• 대한설비공학회:학술대회논문집
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• 대한설비공학회 2008년도 하계학술발표대회 논문집
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• pp.1047-1052
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• 2008

The aim of this paper is that studies on the characteristics of the liquid-gas ejector. Could get data about various model using numerical analysis. Compare and analyze result that get by an experiment and numerical analysis. And studied Characteristics of the ejector. In this paper, Numerical analysis model is gotten divided according to each Throat ratio as three types. Each throat ratio is 0, 4 and 7.5. According to the result that analyze basic model, pressure became lower causing the volume flow rate increase. In CFD studies, Fixed volume flow rate by these result and analyzed ejector performance. As a result, there was no change of pressure to Throat's Enterance, and pressure became low while pass the throat. Since, pressure recovered while passing diffuser. The outer flow velocity did not change greatly to change of volume flow rate. This research expects that is utilized to data for performance elevation hereafter.

• 한국산학기술학회논문지
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• 제15권11호
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• pp.6412-6418
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• 2014

본 논문은 기체-액체 이젝터의 수치해석연구에 초점을 맞추고 있다. 이젝터는 구동유체가 노즐을 통해 고속으로 분출될 때, 구동노즐 출구 주변에 진공압이 형성되어 주변의 기체와 운동량 교환을 통하여 저압의 유체를 보다 높은 압력으로 압축하여 수송하는 장치이다. 기체-액체 이젝터는 상용 소프트웨어 ANSYS-CFX 14.0을 사용하여 다상의 CFD 분석을 통해 연구한다. 구동유체는 물을 사용하여 구동되며, 실제로는 공기가 아닌 오존을 사용하여 배출 된다. 기체-액체 이젝터의 디퓨저의 형상에 따라 성능 차이를 비교한다. 결과 기체-액체 이젝터의 성능에 미치는 다양한 요인을 제공 한다. 그리고 제안 된 수치 모델은 기체-액체 이젝터의의 최적 설계에 매우 도움이 될 것다.

• 한국추진공학회:학술대회논문집
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• 한국추진공학회 2012년도 제38회 춘계학술대회논문집
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• pp.475-478
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• 2012

케로신과 액체산소를 추진제로 하는 로켓엔진의 고공환경모사를 위한 실험 장치의 예비 설계를 수행하였다. 고공환경모사를 위한 장치는 진공챔버, 초음속디퓨저, 열교환기, 이젝터, 증기 발생기로 구성된다. 로켓엔진을 장착한 진공챔버는 이차목 초음속 디퓨저에 의해 고공환경의 압력이 모사되고 이를 유지한다. 로켓엔진의 메인 연소가스는 열교환기에서 물로 냉각되며 이로 인한 혼합물은 이젝터로 인해 대기 중으로 배출된다. 이젝터는 75% 에탄올과 액체산소, 물로 작동하는 증기 발생기에 의해 작동되며 초기 진공도를 유지하는 역할을 한다.